Flash vapor generator and assembly comprising a flash vapor generator

ABSTRACT

The invention relates to a device for generating decontamination agent vapor, in particular hydrogen peroxide vapor, comprising an evaporator body ( 9 ), a heating unit ( 22 ) for heating the evaporator body ( 9 ) and a plurality of feed channels ( 28 ) for feeding decontamination liquid to be evaporated, preferably a liquid containing hydrogen peroxide, to the evaporator body ( 9 ). According to the invention, a plurality of blind holes ( 16 ) are provided in the single- or multi-part evaporator body ( 9 ), and at least one of the feed channels ( 28 ) is assigned to the blind holes ( 16 ).

The invention relates to a device for generating decontamination agent vapour, particularly hydrogen peroxide vapour, comprising an evaporator body, a heating unit for heating the evaporator body and a plurality of feed channels for feeding decontamination liquid to be evaporated, preferably a liquid containing hydrogen peroxide. The invention preferably relates to a so-called flash vapour generator (high-speed vapour generator). The invention further relates to a preferably pharmaceutics-based assembly comprising a space to be decontaminated, particularly an isolator and/or a lock, and a device for generating decontamination agent vapour.

Hydrogen peroxide vapour is used for the decontamination of isolators and/or locks in the pharmaceutical industry, due to its high reactivity. Hydrogen peroxide vapour is obtained by evaporating an aqueous hydrogen peroxide solution. To minimise the explosion risk during the evaporation of solutions containing hydrogen peroxide, so-called flash evaporators (flash vapour generators) are used, with the aim of the continuous, rapid (in a flash) evaporation of small quantities of liquid containing hydrogen peroxide. It is not permitted for larger quantities of liquid containing hydrogen peroxide to be boiled, due to the aforementioned explosion risk. The difficulty in evaporating small quantities of hydrogen peroxide-containing liquid, particularly aqueous solutions, is the formation of liquid droplets which “dance” on hot evaporator surfaces and impede efforts towards rapid evaporation.

A hydrogen peroxide vapour generator with a flat evaporator surface is known from DE 10 2006 006 095 A1. The aforementioned “dancing” droplet formation can take place here.

An alternative flash evaporator (high-speed evaporator) is known from EP 0 972 159 B1, which is characterised by evaporator channels disposed in an evaporator body in a hydraulically interconnecting manner. The design is comparatively complex.

In relation to the further state of the art, reference is made to DE 602 03 603 T2 or DE 603 00 820 T2.

A hydrogen peroxide evaporator with a pot-like housing and an evaporator body is known from DE 2005 030 822 A1, said evaporator having a single, large-scale evaporator surface, wherein heat is supplied to the decontamination agent only from below. The known evaporator seems to be in need of improvement in terms of its evaporation rate and also in relation to the avoidance of “dancing” decontamination agent droplets. It is further known from DE 2005 030 822 A1 for a plurality of evaporators to be connected via one line in each case to a vessel requiring sterilisation, in order to increase the amount of decontamination vapour. The total evaporator costs are therefore incurred x-times. In addition, a plurality of vapour lines must be conducted into the space to be evaporated, which is problematic in the case of small spaces for lack of space. In addition, a plurality of seals must then be provided.

A water evaporator is known from CN 2009 43844 Y. The known evaporator has an evaporator body with a plurality of small holes. A single feed channel is jointly assigned to these, said feed channel being disposed centrally above the evaporator body. So that the plurality of small holes can make their contribution to the evaporation, a sufficiently large quantity of liquid must be fed through the single feed channel, although this would then run counter to the goal of the spontaneous flash evaporation of decontamination agents. In practice, this would result in a hazardous boiling of decontamination agents. The known evaporator is not therefore suitable for evaporating decontamination agents.

All the aforementioned flash evaporators are characterised by a comparatively complex design and/or by an evaporation rate capable of improvement.

Based on the aforementioned state of the art, the problem addressed by the invention is that of indicating a flash evaporator (high-speed evaporator) with the simplest possible design to generate decontamination agent vapour, which is characterised by a high evaporation rate. The formation of “dancing” decontamination agent liquid droplets within the evaporator should preferably be largely avoided. Moreover, the problem involves indicating an assembly comprising a space to be decontaminated and a correspondingly improved vapour generator. This is preferably an assembly for decanting and/or processing pharmaceuticals.

In relation to the high-speed vapour generator, the problem is solved in the case of a generic device, in that a plurality of blind holes is provided in the one-part or multi-part evaporator body and the blind holes are each assigned at least one, preferably exclusively one, of the feed channels, in order to conduct the decontamination agent liquid to be evaporated via these, preferably in droplets. The decontamination liquid to be evaporated is preferably an aqueous solution of hydrogen peroxide, quite especially preferably a 35% to 50% solution.

In relation to the assembly, preferably a pharmaceutical assembly, the problem is solved through the use of a vapour generator designed as described earlier.

Advantageous developments of the invention are specified in the dependent claims. Included within the framework of the invention are all combinations of at least two features disclosed in the description, claims and/or figures. To avoid repetition, features disclosed with respect to the device should also be regarded as disclosed and claimable with respect to the method. Similarly, features disclosed with respect to the method should also be regarded as disclosed and claimable with respect to the device.

The invention is based on the knowledge that rapid evaporation of decontamination liquid fed preferably in droplets can be achieved in relation to the evaporation rate in an improved, simplified manner in that the evaporation takes place within (peripherally closed) blind holes in a one-part or multi-part evaporator body. This is due to, among other things, the fact that the heated peripheral wall of the blind holes is at a significantly smaller distance from the decontamination liquid fed for evaporation than a peripheral wall of a cylindrical evaporator with a level base area. In a high-speed evaporator designed according to the concept of the invention, a larger amount of heat can thereby be fed to the decontamination liquid to be evaporated, preferably fed in droplets, in the shortest possible time, namely not from below, but also through radiation heat from the peripheral wall of the corresponding blind hole. Through the provision of blind holes provided in an evaporator body (particularly an evaporator block), which may be produced as bores for example, an exceptionally simple and effective evaporator device design is achieved. Unlike in the case of evaporators known from the state of the art, it is not necessary to provide evaporator channels crossing the evaporator body, through which the liquid to be evaporated is conducted, wherein the aforementioned channels in the state of the art are also hydraulically interconnected in a costly manner. Quite particularly advantageous is an embodiment of the device for generating decontamination agent vapour, in which the preferably one-part evaporator body is formed from aluminium, particularly an aluminium alloy, to achieve optimum heat conduction. It is still further preferred for the heating unit to be designed and set such that it heats the evaporator body to a temperature within a temperature range of between roughly 100° C. and roughly 140° C. It is quite particularly preferable for the temperature to be around 120° C. or under during evaporator operation, so that the formation of closed, not suddenly evaporating droplets on the evaporator surface is optimally prevented. It is particularly advantageous for the maximum diameter of the blind holes preferably with cylindrical contours at least in section not to exceed a dimension of 50 mm. It is still further preferable for the maximum diameter to be 40 mm or under. It is quite particularly preferable for the diameter to be chosen from a range of values of between roughly 30 mm and 35 mm. Ideally, the maximum depth extension of the blind holes (closed at the bottom) is also limited and amounts to under 50 mm, quite particularly preferably under 40 mm, even more preferably under 30 mm. The depth extension as far as the base of the blind hole is preferably roughly 25 mm.

Particularly preferred is an embodiment in which the blind holes do not have a circular contour, but a rectangular one, particularly, at least approximately, square, wherein it is still further preferred for the blind holes to have no sharp edges, but edges exhibiting a radius, i.e. rounded. This embodiment seems rare at first sight, as blind holes with rectangular contours are comparatively expensive to produce compared with blind holes with circular contours, particularly due to the milling. Surprisingly optimised evaporation properties can be achieved, however, through the rectangular contour (two pairs of parallel sides disposed at right angles), preferably with rounded corners.

It is particularly advantageous for the length to width ratio of the blind holes to be roughly 1 to roughly 1.3, particularly preferably roughly 1.1. In a quite particularly preferred embodiment, the length of each blind hole (measured towards the longitudinal extension of the evaporator) is roughly 27.75 mm and (the width extending perpendicularly thereto) is roughly 25 mm. Particularly preferably, the depth of the blind holes with a rectangular contour is roughly 24 mm. In other words, the ratio between the length, width and depth is approximately 1:1:1. It has proved particularly advantageous for blind holes with a rectangular contour to be disposed in a row. Quite particularly preferably, six identical blind holes are disposed in a row, i.e. behind one another in the longitudinal extension of the evaporator, wherein two adjacent blind holes in each case are spaced from one another by fewer than 10 mm, quiet particularly preferably by roughly 4 mm.

The number of blind holes provided and/or to be supplied with decontamination liquid to be evaporated at the active agent concentration to be reached in the carrier air and/or in the atmosphere of the space to be decontaminated is adapted and adjusted in this manner.

In accordance with the invention at least one, preferably exclusively one feed channel in each case, is allocated to each of the blind holes for the feeding of decontamination agents to be evaporated, particularly in droplets—this means that the feed channels are disposed such that the decontamination agent to be evaporated can be fed straight into the blind holes, preferably dropped into these.

There are different possibilities with regard to the geometric design of the blind holes. Quite particularly preferably, these have a cylindrical casing surface, preferably coupled with a circular base surface. Alternatively, the blind holes may have a cylindrical casing surface coupled with a conical base section.

As previously explained, the blind holes are rectangular according to an alternative embodiment, particularly with an at least approximately square contour, wherein it is still further preferable for the edges running in an upright direction (viewed in the peripheral direction) to be rounded, for example, preferably with a curvature radius of roughly R=5 mm.

In accordance with an alternative embodiment, the diameter of the cross-sectional surface of the blind holes, which preferably have a circular contour, diminishes as the distance from their upper inlet opening increases, alternatively stepped or continuously, for example, conically.

It is particularly preferable for all blind holes to be identically formed.

In a further development of the invention, it is advantageously provided that the blind holes are not immediately adjacent to one another, but are spaced apart from one another, particularly in order thereby to guarantee a uniform heat supply. The blind holes are preferably not hydraulically interconnected directly, via cross-bores for example.

There are also different possibilities with regard to the specific embodiment of the evaporator body. Evaporator bodies known in the art usually have a cylindrical contour. An embodiment in which the evaporator body of the device proposed here for generating decontamination agent vapour has a greater length extension than the width extension and preferably also a greater length extension than the depth extension is preferred. It is quite particularly advantageous for the evaporator body to have at least approximately square contours at least in sections.

There are also different possibilities with regard to the arrangement of the blind holes. An embodiment is preferred in which at least one, preferably exclusively one, row of blind holes extending in the direction of the longitudinal extension of the evaporator body is provided. An embodiment with a plurality of particularly parallel rows can also be achieved.

The heating unit is preferably designed and disposed in such a manner that it extends along the longitudinal sides, i.e. along the longitudinal extension of the evaporator body. It preferably also extends in addition along the base surface. It is quite particularly advantageous where two, particularly parallel, rows of blind holes are provided, if the heating unit extends into an area between the rows, so that a uniform supply of heat to the blind holes can thereby be guaranteed. The heating unit is preferably an electrical resistance heater. A temperature sensor, for example a PT 100, is advantageously included in the evaporator body. The temperature sensor, particularly the PT 100, is preferably used to monitor and record the temperature and the temperature course. Quite particularly preferred in addition to or as an alternative to the temperature sensor, a thermocouple assigned to the heating device is provided. The heating unit is ideally at least a heating rod, which is preferably contained in an opening, particularly a bore, running in the direction of the evaporator's longitudinal extension. The thermocouple is also preferably disposed in this opening, preferably integrally with the heating rod. It is still further preferred for a plurality of heating rods, particularly disposed in parallel, to be provided. Good results were obtained with a total of three heating rods, wherein the three heating rods are preferably controlled by means of a joint thermocouple, which is yet further preferably located in a central bore or opening along with the central heating rod. The use of a total of only two heating rods disposed symmetrically relative to a perpendicular mirror plane is particularly preferred.

To prevent the decontamination liquid conducted through the feed channels from being entrained by carrier air before the liquid is evaporated, provision is advantageously made in a development of the invention for the feed channels to penetrate the inlet openings of the blind holes, in other words to project into the blind holes. It is quite particularly preferred in this case for the preferably dry and heated carrier air to flow over the blind holes and thereby entrain the decontamination agent vapour rising from the blind holes.

It may be that in practice the feed channels become encrusted or are subject to wear. To avoid major repair work, it is therefore advantageously provided in a development of the invention that the feed channels through which the decontamination liquid to be evaporated is conducted to the blind holes, preferably in droplets, to the blind holes, are replaceable, i.e. designed and disposed in an interchangeable manner. Surprisingly, for the formation of the feed channels, injection needles available in bulk and particularly made of stainless steel can be used for this. Said needles are preferably provided with a Luer-Lock connection fitting at their upper ends facing away from the blind holes, via which replaceability and interchangeability can be guaranteed. Particularly preferably, the internal diameter of the feed channels is chosen from a value range of between roughly 0.5 mm and roughly 2 mm.

The feed channels formed particularly by injection needles are preferably disposed in such a way that they supply decontamination liquid to be evaporated to the blind holes from a distributor chamber, so in other words they represent the hydraulic connection between the distributor chamber and the blind hole in each case. For this purpose, the feed channels preferably project into a flow channel for carrier air disposed above the blind holes and therefore above the evaporator body or else they are disposed in said flow channel or preferably penetrate it up to and into the blind holes, in order to prevent an entrainment of as yet unevaporated decontamination liquid with the carrier air, as already described.

An embodiment in which the decontamination liquid to be evaporated can flow to the feed channels via a supply channel in each case is particularly advantageous. Ideally, these supply channels are not flexible lines, but channels introduced into, particularly milled into, a metallic evaporator component. The supply channels are ideally inserted in a cover plate and connect a particularly central supply line to the feed channels. In order to guarantee that the feed channels are each supplied with the same quantity of decontamination agent to be evaporated, a development of the invention advantageously provides that the channels—based on an equal flow cross-section—are equally long, so that the liquid to be evaporated encounters the same flow resistance. The aforementioned supply channels are ideally supplied via a clocked metering pump, particularly disposed outside the actual evaporator. It is particularly advantageous for the supply channels to emerge from one, preferably central, space, which still further preferably is introduced as a recess in the cover plate with the supply channels. The supply channels may be sealed by a joint closing plate, for example, which can be secured to the cover plate by screws, for instance. In addition or alternatively, the supply channels may be sealed on their upper side by metal plates, particularly stainless steel plates, wherein said plates are preferably welded to the cover plate exhibiting the supply channels.

It is particularly advantageous if the flow volume of decontamination liquid to be evaporated can be set for the individual feed channels. In other words, it is preferable for at least some of the feed channels to be assigned a setting mechanism with which the flow volume that is to flow through the feed channel can be set. These setting mechanisms are preferably located within or close to the aforementioned distributor chamber, into which decontamination liquid to be evaporated can preferably be pumped from a store, particularly an interchangeable storage bottle.

The invention also relates to an assembly, particularly a pharmaceutical assembly, comprising a space to be decontaminated with decontamination agent vapour, particularly an isolator and/or a lock, and also a device designed as described earlier for generating decontamination agent vapour, particularly hydrogen peroxide vapour.

In the state of the art, high-speed evaporators are customarily disposed in such a manner that they are supplied with air from the space being decontaminated as carrier air and the carrier air enriched with hydrogen peroxide is released straight back into the space to be decontaminated. This usually leads to condensation of hydrogen peroxide in the space being decontaminated. Condensation of this kind should be prevented wherever possible in developments of the invention, which can be advantageously supported or achieved in that the high-speed evaporator is not, or not exclusively, supplied with carrier air from the space to be decontaminated, but with fresh air. Fresh air does not only mean preferably dry ambient air (particularly<10% relative atmospheric humidity), but also compressed air from corresponding storage vessels, particularly pressure cylinders. It is essential that this is not air fed from the space to be decontaminated. This requires air also to be continuously delivered from the space to be decontaminated into the environment, for example, in order to prevent inadmissible overpressures. The advantage of an assembly of this kind is the improved controllability of the hydrogen peroxide concentration in the ambient air of the space to be decontaminated and better pressure controllability during decontamination. The pressure in the space should be above ambient pressure during decontamination, preferably around 30 Pa above it. In relation to the specific configuration of the evaporator, there are two different possibilities here. The evaporator may, for example, be connected to the single fresh air supply line (carrier air supply line), so that all the air to be fed into the space to be decontaminated flows straight through the evaporator. It is preferable for the evaporator to be arranged in this way, if the fresh air supply does not exceed 80 m³ per hour during operation of the space to be decontaminated, particularly an isolator. In an alternative assembly, a bypass line is allocated to the preferably single fresh air line (supply line) disposed in the flow direction upstream of the evaporator, the evaporator being connected to said bypass line—this results in part of the fresh air supplied not passing directly through the evaporator, but preferably being mixed with the diverted enriched carrier air passing through the evaporator before it reaches the space to be decontaminated. An assembly of this kind is particularly appropriate when the space to be decontaminated is in operation, i.e. following decontamination of a fresh air supply of over 80 m³ per hour.

To set or control the decontamination agent vapour concentration in the carrier air, it is preferable for a regulation line to discharge into an intermediate or connection line downstream of the evaporator, through which an adjustable volume of air, particularly of fresh air, can be mixed to dilute the vapour concentration in the carrier air.

Further advantages, features and details of the invention emerge from the following description of preferred embodiments and also using the drawings. In the drawings:

FIG. 1 shows a perspective view of a device for generating decontamination agent vapour (high-speed evaporator, flash evaporator),

FIG. 2 to FIG. 5 show different sectional views of the device according to FIG. 1,

FIG. 6 shows a representation of an alternative evaporator,

FIG. 7 to FIG. 10 show different sectional views of the device according to FIG. 6,

FIG. 11 shows a pharmaceutical assembly in a highly schematic form, comprising an isolator and a high-speed evaporator, wherein the single fresh air supply line is connected straight to the evaporator,

FIG. 12 shows an alternative pneumatic assembly, in which the evaporator is disposed in a bypass line in a fresh air line,

FIG. 13 shows a further alternative embodiment of an evaporator in an exploded view,

FIG. 14 a to FIG. 14 e show the evaporator body of the evaporator according to FIG. 13 in different, partially sectional views,

FIG. 15 a to FIG. 15 e show different, partially sectional views of a closing plate for securing the cover plate shown in FIG. 16 a to FIG. 16 e and

FIG. 16 a to FIG. 16 e show a cover plate of the evaporator in accordance with FIG. 13 with supply channels of equal length introduced into said plate.

Identical elements and elements with the same function are labelled in the figures using the same reference numbers.

FIG. 1 shows a first exemplary embodiment of a device 1 (high-speed evaporator, flash evaporator) for generating decontamination agent vapour, in this case hydrogen peroxide vapour for decontaminating a pharmaceutical packing device for drugs (not shown) disposed in an isolator.

The device 1 comprises a connector 3 for carrier air at a first end 2 for transporting away the decontamination agent vapour generated to a space to be decontaminated which is not shown. At the second end 4 (cf. FIG. 2) facing away from the first end 2, there is a connection not represented in FIG. 1 for connecting a connection line leading to the space to be decontaminated. The connections can be screwed into a lower device section 5 or into holes with an internal thread 6, 7 introduced therein.

A free cross-section, i.e. a flow channel 8, is realised axially between the connections, through which the carrier air, in this case fresh air, for example compressed air or ambient air, flows and can thereby take the decontamination agent vapour with it.

The lower device section 5 comprises a metallic evaporator body 9 made of an aluminium alloy. As emerges from FIG. 1, the width extension b of said lower device section is significantly smaller than its length extension I, the width extension b roughly corresponding to the height extension h. As can be further deduced from the figures, the evaporator body 9 is prismatic in form and is formed integrally with the metallic casing of the flow channel 8 disposed above it in the exemplary embodiment shown. An upper device section 11 is screwed to the lower device section 5 in a cover-type manner, wherein the upper device section 11 comprises a distributor chamber 12 in which decontamination liquid to be evaporated, particularly an aqueous, preferably 35% hydrogen peroxide solution, can be supplied via a connection closed by means of a transport screw 13 in the exemplary embodiment shown.

Two rows 14, 15 of blind holes 16, i.e. holes only open at one end, separate and spaced apart from one another are introduced into the evaporator body 9 in the exemplary embodiment shown. The blind holes 16 and recesses are separate from one another, i.e. they are not directly hydraulically interconnected and extend perpendicularly to the carrier air flow direction and therefore perpendicularly to the solution extension of the evaporator body 9. As emerges particularly from FIG. 4, the cross-sectional surface of the blind holes 16 diminishes starting from an inlet opening 17 as far as a blind hole base 18. In the exemplary embodiment shown, the blind holes 16 are executed as a multi-stage stepped bore for this purpose, wherein a conical contour is also attainable as an alternative. As will be explained later with reference to FIG. 5, the flow channel 8 is crossed by needle-like feed channels running perpendicular to its longitudinal extension, through which decontamination liquid to be evaporated from the distributor chamber 12 is conducted in droplets to the individual blind holes 16. In this case, the feed channels arranged so as to be interchangeable cross the inlet openings 17, so that the carrier air flowing through the flow channel 8 cannot entrain them.

It emerges from FIG. 3 that the evaporator body 9 is surrounded at its base end 19 and also on both longitudinal sides 20, 21 by a heating unit 22, in this case an electrical heating unit, adjacent to the evaporator body 9, said heating device being controllable such that the evaporator body reaches a temperature of roughly 110° C. in the exemplary embodiment shown. The actual temperature can be measured using a temperature sensor 23, which can be inserted in a bore 24 extending in the direction of the longitudinal extension of the evaporator body 9.

It emerges from FIGS. 1, 2 and 3 that the lower evaporator section 5 offers a peripheral securing flange at its upper end, which rests on the upper device section 11 with a corresponding counter-flange 26 and is screwed down.

FIG. 5 shows the mounted device 1 in a longitudinal sectional view. The upper central connection 27 for a feed line for feeding decontamination liquid to be evaporated into the flat distributor chamber 12 can be identified. To create the distributor chamber 12, the upper device section 11 and the housing walls thereof have a two-piece design.

As further emerges from FIG. 5, each blind hole bore 16 is allocated a single feed channel 28 designed and disposed in an interchangeable manner, which is formed in each case by a stainless steel injection needle in the exemplary embodiment shown. Said injection needle exhibits a Luer-Lock connection piece 29 on its upper section, with which it can be fixed to a corresponding adapter 30 on the upper device section 11 beneath the distributor chamber 12. For reasons of clarity, only a single feed channel 28 with the associated adapter 30 is represented—in reality, an adapter 30 of this kind with an associated feed channel 28 is allocated to each blind hole 16. It is clear that the feed channel 28 crosses the flow channel 8 perpendicularly to it longitudinal extension and enters the blind hole 16 beneath the inlet opening 17. A setting screw 31 is assigned to each feed channel 28, with which the volume of liquid flowing through the feed channel 28 as far as the respective blind hole 16 can be set.

The device 1 depicted in FIGS. 6 to 10 basically corresponds to the device shown in FIGS. 1 to 5 and previously described. To avoid repetition, only the differences are essentially dealt with in the following—with regard to similarities, reference is made to FIG. 1 with the associated figure description.

Unlike the previously described exemplary embodiment, the evaporator body 9 of the device 1 in accordance with FIGS. 6 to 10 only comprises a single row 14 of blind holes 16. These are not executed conically or as stepped bores, but comprise a cylindrical casing surface 32, wherein the blind hole base 18 is preferably circular in form, as illustrated—to simplify manufacture, however, it is also conceivable for a conical blind hold base to be executed. In the exemplary embodiment shown, a total of six blind holes are provided. Quite particularly preferred is the execution of only five blind holes, wherein it is quite particularly preferred for a single feed channel 28, preferably formed by an injection needle, to be allocated to each blind hole 16.

In the interests of clarity, FIG. 10 once again shows only a single feed channel 28, wherein each blind hole is assigned its own feed channel 28, in this case provided with a Luer-Lock connection piece, which is interchangeably held in an associated adapter 30.

FIG. 11 shows an assembly 33, in this case a pharmaceutical assembly, comprising a space 34 to be decontaminated in the form of an isolator, only represented in highly schematic form, said space comprising an inlet connection 35 and an outlet connection 36. A filter 37, in this case a so-called Hepa filter, is assigned to the inlet connection 35, to filter the incoming carrier air enriched with decontamination agent vapour. In an alternative embodiment which is not shown, decontamination agent vapour can be fed straight into the space, i.e. not via the filter. A device 1 (high-speed evaporator) is connected straight to the single fresh air line 38 disposed upstream of the device 1 in the flow direction, so that the total air flowing in through the fresh air line 38 flows through the device 1 and is thereby enriched with decontamination agent vapour. The carrier air (fresh air) can be preheated by means of a temperature-regulating mechanism 39. The fresh air may come from a bottle of compressed gas, for example, or be drawn in from the environment, wherein in the latter case an air drying mechanism is preferably provided. In the flow direction downstream of the device 1, a regulating line 41 discharges into the line 40 (intermediate line) for the controlled feed of additional fresh air to adjust the decontamination vapour concentration in the carrier air to be fed to the space 34. A discharge line 42 is connected to the outlet connection 36, in which a filter 43, in this case a Hepa filter, is connected, across which the waste air can flow into the environment or to a catalytic converter in order for the hydrogen peroxide vapour to be broken down.

The assembly 33 in accordance with FIG. 12 essentially corresponds to the assembly in accordance with FIG. 11. To avoid repetition, the differences are basically dealt with in the following text. With regard to the similarities, reference is made to FIG. 11 with the associated description of figures.

It is evident that the device 1 (high-speed evaporator) is connected to a bypass line 44 to conduct fresh air 38, so that not all fresh air supplied flows through the device 1. As in the exemplary embodiment according to FIG. 11, the decontamination principle is based on so-called fresh air decontamination—this means that only air not originating in the space 34 to be decontaminated, i.e. enriched with hydrogen peroxide vapour, is fed to the device 1, but fresh air, i.e. compressed air or particularly dried ambient air.

FIG. 13 shows an alternative exemplary embodiment of a device 1 (high-speed evaporator, flash evaporator) for generating decontamination agent vapour, in this case hydrogen peroxide vapour, for decontaminating a pharmaceutical isolator.

The device 1 comprises an evaporator body 9 with a trough-like form in an upper section and a prismatic form in a lower section, wherein the upper section laterally encloses a flow channel 8. A cover plate 45, which seals the top of the flow channel 8 in the mounted state, may be fastened to the evaporator body 9 by screws. Supply channels 46 to be commented on later are introduced into the cover plate 45, in this case by milling. The supply channels 46 transport decontamination liquid to be evaporated to adapters 30 for interchangeable supply channels 28. Said supply channels take the form of injection needles made of stainless steel and have a Luer-Lock connection 29 at their upper end for fixing in an adapter 30 in each case.

In the exemplary embodiment shown, the sealing plate 47 which can be screwed to the cover plate 16 closes the groove-like supply channels 46 from above. In addition or alternatively, the supply channels 46 may be closed with an upper wall, preferably welded on subsequently, particularly made of stainless steel.

The supply channels 46 emerge from a central recess 48 (space), into which decontamination liquid to be evaporated is fed by means of a clocked metering pump (not shown) via a supply line.

As can be further seen from FIG. 13, three parallel bores 24 extending in the direction of the longitudinal extension of the evaporator body 9 are introduced into the evaporator body 9 in an area beneath the blind holes 16 which are to be commented on later. A heating rod 49 may be inserted in each bore 24. The heating rods 49 create the heating unit 22. Casing (jacket) heating is preferably dispensed with in this embodiment. The centre heating rod 49 is preferably assigned a thermocouple which is not shown, with which the three heating rods 49 can be controlled. In addition, a PT 100 (temperature sensor 23) is shown in FIG. 13, which can be inserted into an opening 50 transversely above the centre bore 24.

FIGS. 14 a to 14 c show different representations of the evaporator body 9 in accordance with the exemplary embodiment in FIG. 13. A top view shows blind holes 16 with a rectangular, in this case approximately square, contour, wherein a total of six blind holes are disposed in a row. The ratio between the blind hole length, the blind hole width and the blind hole depth is roughly 1:1:1. The blind hole length is 27.75 mm, the blind hole width 25 mm and the blind hole depth 24 mm. As can be seen from FIG. 14 b, the corners (edges 51) of the blind holes 16 are rounded in design. Each blind hole 16 is assigned a replaceable feed channel 28 shown in FIG. 13. In the exemplary embodiment according to FIG. 13 to FIG. 16 d, the feed channels 28 project into the respective blind hole 16, thereby crossing the flow channel 8, so as to prevent an entrainment of liquid droplets.

FIGS. 15 a to 15 e show the sealing cover 47. This exhibits a central feed 52, through which the decontamination liquid to be evaporated reaches the evaporator. As can be seen from FIG. 15 d, the feed 52 is in the form of a hole with an internal thread, so that a corresponding flexible feed line (supply line) or an adapter for a flexible line of this kind can be secured.

In addition, six internally threaded holes 53 disposed in a row are provided, wherein an internally threaded hole of this kind is assigned to each feed channel 28 (cf. FIG. 13). These each include a set screw (not shown) to adjust the quantity of decontamination liquid being supplied. The set screw is not shown in the interests of clarity.

FIGS. 16 a to 16 e show the cover plate 45 shown in FIG. 13, onto which the sealing plate 47 shown in FIGS. 15 a to 15 e can be screwed, in order to seal the supply channels 46 inserted in the cover plate 45. All supply channels are the same length and have the same channel cross-section. The supply channels 46 emerge from a recess 48, which is disposed beneath the feed 52 in the assembled state. Decontamination liquid to be evaporated may flow from the recess 48 via the supply channels 46 to the feed channels 28 (cf. FIG. 13). In order to achieve an equal length for the supply channels 46, these are differently formed, in some cases with a change of direction. The supply channels 46 have a rectangular cross-section in the exemplary embodiment shown (cf. FIG. 16 c). In the assembled state, the cover plate 45 seals the flow channel 8 for fresh air, for example compressed air or dried ambient air. The fresh air preferably has a relative humidity below 10%.

REFERENCE LIST

-   1 Device -   2 First end -   3 Connection -   4 Second end -   5 Lower device section -   6 Internally threaded hole -   7 Internally threaded hole -   8 Flow channel -   9 Evaporator body -   10 Casing -   11 Upper device section -   12 Distributor chamber -   13 Transport screw -   14 Row -   15 Row -   16 Blind hole -   17 Inlet opening -   18 Blind hole base -   19 Base end -   20 Longitudinal side -   21 Longitudinal side -   22 Heating unit -   23 Temperature sensor -   24 Bore -   25 Securing flange -   26 Counter-flange -   27 Connection -   28 Feed channel -   29 Luer-Lock connection piece -   30 Adaptor -   31 Set screw -   32 Cylinder jacket surface -   33 Assembly -   34 Space to be decontaminated -   35 Inlet connection -   36 Outlet connection -   37 Filter -   38 Fresh air line -   39 Temperature control mechanism -   40 Line -   41 Regulating line -   42 Discharge line -   43 Filter -   44 Bypass line -   45 Cover plate -   46 Supply channels -   47 Sealing plate -   48 Recess -   49 Heating rods -   50 Opening -   51 Edges -   52 Feed -   53 Internally threaded holes 

1. A device for generating decontamination agent vapour, particularly hydrogen peroxide vapour, comprising an evaporator body (9), a heating unit (22) for heating the evaporator body (9) and a plurality of feed channels (28) for feeding decontamination liquid to be evaporated, preferably a liquid containing hydrogen peroxide, to the evaporator body (9), characterised in that a plurality of blind holes (16) is provided in the one-part or multi-part evaporator body (9) and the blind holes (16) are each assigned at least one of the feed channels (28) and that the feed channels are disposed in such a manner that the decontamination agent liquid to be evaporated can be dropped straight into the blind holes (16).
 2. The device according to claim 1, characterised in that the cross-sectional surface of the blind holes (16) is constant, at least in terms of the axial section, preferably at least over the largest part of the axial extension thereof, preferably over the entire axial extension thereof.
 3. The device according to claim 1 or 2, characterised in that the cross-sectional surface of the blind holes (16) has an at least approximately rectangular, particularly square, contour, preferably with rounded corners.
 4. The device according to claim 1, characterised in that the cross-sectional surface of the blind holes (16), preferably with a circular contour, at least in terms of the axial section, diminishes continuously, preferably conically, and/or in a stepped manner as the distance from the inlet opening (17) increases.
 5. The device according to one of the preceding claims, characterised in that the blind holes (16) are spaced apart from one another.
 6. The device according to one of the preceding claims, characterised in that the evaporator body (9), which is prismatic preferably at least in sections, has a length extension greater than its width extension.
 7. The device according to one of the preceding claims, characterised in that the blind holes (16) are disposed in at least one row (14, 15) extending in the direction of the longitudinal extension of the evaporator body (9).
 8. The device according to one of the preceding claims characterised in that the heating unit (22) extends along two longitudinal sides (20, 21) of the evaporator body (9) facing away from each other and/or along a lower base surface and/or along an intermediate plane disposed between two rows of blind holes (14, 15).
 9. The device according to one of the claims 1 to 7, characterised in that at least one heating rod (29), preferably three heating rods (49), is/are provided as the heating unit (22), said heating rod being contained in a longitudinal opening (50) in the evaporator body (9).
 10. The device according to one of the preceding claims characterised in that the preferably rigid, preferably metallic feed channels (28), particularly made of stainless steel, are disposed projecting into the blind holes (16).
 11. The device according to one of the preceding claims characterised in that the feed channels (28) are designed and disposed in an interchangeable manner.
 12. The device according to one of the preceding claims characterised in that the feed channels (28) are formed from injection needles preferably exhibiting one Luer-Lok connection piece (29) in each case.
 13. The device according to one of the preceding claims characterised in that a distributor chamber (12) spaced apart from the evaporator body (9) via a flow channel (8) for carrier air is assigned to the feed channels (28).
 14. The device according to one of the preceding claims, characterised in that a preferably milled supply channel (46) is assigned to each feed channel (28), wherein the supply channels (46) are preferably the same length and have the same flow cross-section and still further preferably can be supplied by a common supply line.
 15. The device according to one of the preceding claims characterised in that the flow volume of the feed channels (28) can be adjusted, preferably by a set screw (31) in each case.
 16. An assembly comprising a space (34) to be decontaminated, particularly an isolator and/or a lock, and a device (1) for generating decontamination agent vapour, particularly hydrogen peroxide vapour, according to one of the preceding claims.
 17. An assembly according to claim 16, characterised in that the device (1) is disposed such that it can be supplied, preferably exclusively, with fresh air, particularly compressed air or ambient air, as the carrier air from outside the space to be decontaminated (34).
 18. An assembly according to claim 16, characterised in that the device is connected to a bypass line (44) to a fresh air line (38) or straight to a fresh air line (38). 